KR19980086762A - Deposition chamber and method for depositing a film having low dielectric constant - Google Patents
Deposition chamber and method for depositing a film having low dielectric constant Download PDFInfo
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- KR19980086762A KR19980086762A KR1019980016047A KR19980016047A KR19980086762A KR 19980086762 A KR19980086762 A KR 19980086762A KR 1019980016047 A KR1019980016047 A KR 1019980016047A KR 19980016047 A KR19980016047 A KR 19980016047A KR 19980086762 A KR19980086762 A KR 19980086762A
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- 230000008021 deposition Effects 0.000 title claims abstract description 46
- 238000000151 deposition Methods 0.000 title claims description 53
- 238000000034 method Methods 0.000 title claims description 34
- 239000007789 gas Substances 0.000 claims abstract description 128
- 239000000758 substrate Substances 0.000 claims abstract description 74
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 65
- 239000001301 oxygen Substances 0.000 claims abstract description 65
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 65
- 230000008569 process Effects 0.000 claims description 18
- 238000012545 processing Methods 0.000 claims description 12
- 239000012530 fluid Substances 0.000 claims description 10
- 230000006698 induction Effects 0.000 claims description 4
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 abstract description 48
- 229910000077 silane Inorganic materials 0.000 abstract description 48
- 239000000203 mixture Substances 0.000 abstract description 8
- 238000009827 uniform distribution Methods 0.000 abstract description 3
- 239000012528 membrane Substances 0.000 abstract description 2
- 239000010408 film Substances 0.000 description 40
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 10
- 229910052731 fluorine Inorganic materials 0.000 description 10
- 239000011737 fluorine Substances 0.000 description 10
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 6
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 6
- 229910052710 silicon Inorganic materials 0.000 description 6
- 239000010703 silicon Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000004065 semiconductor Substances 0.000 description 5
- 238000004544 sputter deposition Methods 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 229910052814 silicon oxide Inorganic materials 0.000 description 4
- 229910004018 SiF Inorganic materials 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000005229 chemical vapour deposition Methods 0.000 description 3
- 229910052736 halogen Inorganic materials 0.000 description 3
- 150000002367 halogens Chemical class 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000005268 plasma chemical vapour deposition Methods 0.000 description 3
- 239000000376 reactant Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- -1 chamber pressure Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229940104869 fluorosilicate Drugs 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000009616 inductively coupled plasma Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000001465 metallisation Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000012495 reaction gas Substances 0.000 description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910020177 SiOF Inorganic materials 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000003491 array Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004590 computer program Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003989 dielectric material Substances 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 239000002019 doping agent Substances 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000005368 silicate glass Substances 0.000 description 1
- ABTOQLMXBSRXSM-UHFFFAOYSA-N silicon tetrafluoride Chemical compound F[Si](F)(F)F ABTOQLMXBSRXSM-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000002230 thermal chemical vapour deposition Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/20—Deposition of semiconductor materials on a substrate, e.g. epitaxial growth solid phase epitaxy
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45563—Gas nozzles
- C23C16/45574—Nozzles for more than one gas
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- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
- C23C16/30—Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
- C23C16/40—Oxides
- C23C16/401—Oxides containing silicon
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- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45512—Premixing before introduction in the reaction chamber
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45514—Mixing in close vicinity to the substrate
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45563—Gas nozzles
- C23C16/45576—Coaxial inlets for each gas
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
- H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
- H01J37/32—Gas-filled discharge tubes
- H01J37/32431—Constructional details of the reactor
- H01J37/3244—Gas supply means
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Abstract
개선된 증착 챔버(2)는 기판 지지대(14)를 하우징하는 챔버(18)를 한정하는 하우징(4)을 포함한다. 산소와 SiF4의 혼합물은 제 1 노즐 세트(34)를 통해 이송되고 실란은 제 2 노즐 세트(34a)를 통해 기판 지지대의 주변(40) 둘레의 챔버내로 이송된다. 실란(또는 실란과 SiF4의 혼합물)과 산소는 개별적으로 구멍(64, 76)으로부터 기판에 걸쳐 일반적으로 중심적으로 챔버내에 주입된다. 각각의 가스에 대한 최적 흐름 속도의 사용과 결합된 가스의 균일한 분배는 막에 걸쳐 균일하게 낮은 유전 상수(3.4 이하)를 초래한다.The improved deposition chamber 2 comprises a housing 4 defining a chamber 18 housing the substrate support 14. The mixture of oxygen and SiF 4 is conveyed through the first nozzle set 34 and the silane is conveyed through the second nozzle set 34a into the chamber around the perimeter 40 of the substrate support. Silane (or a mixture of silane and SiF 4 ) and oxygen are injected into the chamber, generally centrally, across the substrate from the holes 64, 76. Uniform distribution of the gas combined with the use of the optimum flow rate for each gas results in a uniformly low dielectric constant (below 3.4) across the membrane.
Description
본 발명은 낮은 유전 상수를 갖는 막을 증착하기 위한 증착 챔버 및 그 방법에 관한 것이다.The present invention relates to a deposition chamber and method for depositing a film having a low dielectric constant.
현대 반도체 소자의 제조에서 중요한 단계 중 하나는 가스의 화학 반응에 의해 반도체 기판 상에 박막을 형성하는 것이다. 이런 증착 공정은 화학 기상 증착(CVD)으로서 인용된다. 일반적인 열적 CVD 공정은 열 유도된 화학 반응이 요구된 막을 형성하도록 발생할 수 있는 기판 표면에 반응 가스를 공급한다. 플라즈마 CVD 공정은 기판 표면에 근접하는 반응대에 무선 주파수(RF) 에너지의 적용에 의해 반응 가스의 여기 및/또는 해리를 증진시켜 높은 반응성 종(species)의 플라즈마를 형성한다. 방출된 종의 높은 반응성은 발생할 화학 반응에 필요한 에너지를 감소시키고, 그러므로 CVD 공정에 요구되는 온도를 더 낮춘다.One of the important steps in the fabrication of modern semiconductor devices is the formation of thin films on semiconductor substrates by chemical reaction of gases. This deposition process is referred to as chemical vapor deposition (CVD). Typical thermal CVD processes supply reactant gas to the substrate surface, which can occur to form films in which thermally induced chemical reactions are required. The plasma CVD process promotes excitation and / or dissociation of the reactant gas by the application of radio frequency (RF) energy to a reaction zone proximate the substrate surface to form a plasma of highly reactive species. The high reactivity of the released species reduces the energy needed for the chemical reactions to occur and therefore lowers the temperature required for the CVD process.
플라즈마 CVD 챔버의 디자인 중 하나에서, 진공 챔버는 일반적으로 캐소드로서 기능하고 하부를 따르는 평면 기판 지지대, 상부를 따르는 평면 애노드, 하부로부터 위쪽으로 연장하는 상대적으로 짧은 측벽, 및 상부와 측벽을 접속하는 유전체 돔에 의해 한정된다. 유도 코일이 돔 둘레에 장착되어 소스 무선 주파수(SRF : source radio frequency) 발생기에 접속된다. 애노드와 캐소드는 전형적으로 바이어스 무선 주파수(BRF : bias radio frequency) 발생기에 결합된다. SRF 발생기로부터 유도 코일에 인가된 에너지는 챔버내에 유도성 결합 플라즈마를 형성한다. 이런 챔버는 고밀도 플라즈마 CVD(HDP-CVD: high density plasma CVD) 챔버로서 참조된다.In one of the designs of the plasma CVD chamber, the vacuum chamber generally functions as a cathode and has a flat substrate support along the bottom, a planar anode along the top, a relatively short sidewall extending upward from the bottom, and a dielectric connecting the top and sidewalls. Defined by the dome. An induction coil is mounted around the dome and connected to a source radio frequency (SRF) generator. The anode and cathode are typically coupled to a bias radio frequency (BRF) generator. The energy applied from the SRF generator to the induction coil forms an inductively coupled plasma in the chamber. This chamber is referred to as a high density plasma CVD (HDP-CVD) chamber.
일부 HDP-CVD 챔버에서, 노즐과 같이 균등하게 일정 간격 배치되고 기판 지지 표면의 에지 위의 영역내로 연장되는 2개 이상의 분배기 세트를 측벽에 장착하는 것이 전형적이다. 각각의 분배기 세트에 대한 가스 노즐은 상기 세트에 대한 공통 매니폴드에 결합되고; 매니폴드는 가스 노즐에 처리 가스를 제공한다. 챔버내로 유입된 가스의 구성은 주로 기판에 형성될 재료의 형태에 의존한다. 예를 들면, 플루오로실리케이트 글라스(FSG) 막이 챔버내에서 증착될 때, 처리 가스는 실란(SiH4), 실리콘 테트라플루오르화물(SiF4), 산소(O2) 및 아르곤(Ar)을 포함할 수 있다. 가스 노즐 세트는 일반적으로 다른 가스가 공통 매니폴드를 통해 공통 노즐 세트로 운반될 수 있는 동안 다른 가스와는 개별적으로 챔버내로 약간의 가스를 유입하는 것이 바람직하기 때문에 사용된다. 예를 들면, 상기 FSG 처리에서 O2와 SiF4가 서로 쉽게 운반될 수 있는 동안 O2와는 개별적으로 SiH4를 유입하는 것이 바람직하다. 상기 노즐 팁은 기판 지지대의 주변 둘레 상에 일정 간격 배치되고 그것을 통해 처리 가스가 흐르는 출구, 전형적으로 구멍을 가진다.In some HDP-CVD chambers, it is typical to mount two or more distributor sets on the sidewalls spaced evenly, such as nozzles, and extending into an area above the edge of the substrate support surface. A gas nozzle for each distributor set is coupled to a common manifold for the set; The manifold provides process gas to the gas nozzle. The composition of the gas introduced into the chamber depends primarily on the type of material to be formed on the substrate. For example, when a fluorosilicate glass (FSG) film is deposited in the chamber, the process gas may include silane (SiH 4 ), silicon tetrafluoride (SiF 4 ), oxygen (O 2 ), and argon (Ar). have. Gas nozzle sets are generally used because it is desirable to introduce some gas into the chamber separately from other gases while other gases can be carried through the common manifold to the common nozzle set. For example, O 2 than individually, it is preferred to introduce the SiH 4, while in the FSG process is O 2 and SiF 4 can be easily carried together. The nozzle tip has an outlet, typically a hole, disposed at regular intervals on the perimeter of the substrate support and through which the processing gas flows.
소자 크기가 더 작아지고 집적 밀도가 증가함에 따라, 반도체 제조업자의 처리 요구에 부합하여 처리 기술의 발전이 요구된다. 이런 처리에서 중요한 하나의 파라미터는 막 증착 균일도이다. 무엇보다도 높은 막 균일도를 달성하기 위하여, 증착 챔버내로의 웨이퍼 표면에 걸친 가스 운반을 정확히 제어하는 것이 필요하다. 이상적으로, 웨이퍼 표면에 따라 여러 지점에서 유입되는 가스 비율(예를 들면, O2대 (SiH4+SiF4)의 비율)이 동일해야 한다.As device sizes become smaller and integration densities increase, the development of processing technologies is required to meet the processing needs of semiconductor manufacturers. One parameter important in this process is the film deposition uniformity. Above all, to achieve high film uniformity, it is necessary to precisely control the gas transport across the wafer surface into the deposition chamber. Ideally, the ratio of gas introduced at several points (eg, the ratio of O 2 to (SiH 4 + SiF 4 )) should be the same depending on the wafer surface.
도 1은 이미 개시된 챔버와 같은 종래 증착 챔버에 대한 전형적인 도핑되지않은 실리케이트 글라스(USG) 증착 두께 변화 플롯(46)을 도시한다. 평균 두께는 기준선(48)에 의해 도시된다. 플롯(46)에 의해 알 수 있는 바와 같이, 기판(20)의 주변(42)에 대응하는 플롯(46)의 끝점(50과 52)에서 상대적으로 가파르게 증가하고 있다. 또한 플롯(46)의 중앙(54)은 실질적으로 급강하한다.1 shows a typical undoped silicate glass (USG) deposition thickness variation plot 46 for a conventional deposition chamber, such as the chamber already disclosed. The average thickness is shown by the baseline 48. As can be seen by the plot 46, it is increasing relatively steeply at the endpoints 50 and 52 of the plot 46 corresponding to the perimeter 42 of the substrate 20. In addition, the center 54 of the plot 46 substantially descends.
95년 12월 13일에 제출된 미국 특허 출원 제08/571,618호는 제 3 가스 제어기(60)와 제 3 가스 공급 라인(62)을 통해 제 3 가스 소스(58)에 결합된 중앙 노즐(56)의 사용으로 플롯(46)이 개선되는 방법을 개시한다. 중앙 노즐(56)은 기판지지용 표면(16) 상에 중심적으로 배치된 구멍(64)을 가진다. 중앙 노즐(56)의 사용은 도 1의 USG 증착 두께 변화 플롯(46)으로부터 도 2의 바람직한 플롯(68)으로의 변형을 허용한다. 바람직한 증착 두께 변화 플롯(68)은 증착 두께의 표준 편차가 1 시그마의 1 내지 2%가 될 수 있을 만큼 충분히 평탄하다. 이것은 주로 끝점(50, 52)에서 플롯의 가파른 기울기를 감소하고, 플롯(46)의 중앙(54)에서의 하부 위치에서 상승시킴으로써 달성된다.US patent application Ser. No. 08 / 571,618, filed December 13, 95, discloses a central nozzle 56 coupled to a third gas source 58 via a third gas controller 60 and a third gas supply line 62. Discloses how the plot 46 is improved. The central nozzle 56 has a hole 64 centered on the substrate support surface 16. The use of the central nozzle 56 allows a variation from the USG deposition thickness change plot 46 of FIG. 1 to the preferred plot 68 of FIG. 2. The preferred deposition thickness change plot 68 is flat enough that the standard deviation of the deposition thickness can be 1 to 2% of one sigma. This is mainly achieved by reducing the steep slope of the plot at the endpoints 50, 52 and raising it at a lower position at the center 54 of the plot 46.
3개, 4개, 또는 그 이상의 금속층이 반도체 상에 형성되는 멀티 레벨 금속 기술의 도래로, 반도체 제조의 다른 목표는 금속간 유전체층과 같은 유전체층의 유전 상수를 낮추는 것이다. 낮은 유전 상수 막은 특히 상호 접속 금속화 공정의 RC 시간 지연을 감소하고, 금속화 공정의 서로 다른 레벨 사이의 혼선을 방지하며, 소자 전력 소모를 감소하기 위해 금속간 유전체(IMD) 층으로 바람직하다.With the advent of multi-level metal technology in which three, four, or more metal layers are formed on a semiconductor, another goal of semiconductor fabrication is to lower the dielectric constant of dielectric layers, such as intermetallic dielectric layers. Low dielectric constant films are particularly desirable as intermetal dielectric (IMD) layers to reduce the RC time delay of interconnect metallization processes, prevent crosstalk between different levels of metallization processes, and reduce device power consumption.
낮은 유전 상수를 달성하려는 많은 시도가 진행되어 왔다. 가장 장래성 있는 해결책 중 하나는 플루오르 또는 다른 할로겐 원소(예를 들어 염소 또는 브롬)를 실리콘 산화물층내에 혼합시키는 것이다. 플루오르가 전체 SiOF 망상 조직의 분극화를 감소시키는 음성 원자이기 때문에 실리콘 산화막을 위한 바람직한 할로겐 도판트인 플루오르가 실리콘 산화막의 유전 상수를 낮추는 것으로 믿어진다. 플루오르 도핑된 실리콘 산화막은 플루오르 실리케이트 글라스(FSG) 막으로서 참조된다.Many attempts have been made to achieve low dielectric constants. One of the most promising solutions is to mix fluorine or other halogen elements (eg chlorine or bromine) in the silicon oxide layer. Since fluorine is a negative atom that reduces the polarization of the entire SiOF network, it is believed that fluorine, which is a preferred halogen dopant for silicon oxide, lowers the dielectric constant of the silicon oxide film. The fluorine doped silicon oxide film is referred to as a fluorosilicate glass (FSG) film.
상기한 바와 같이, FSG 막과 같은 감소된 유전 상수를 가지는 산화막을 제조하는 것이 바람직하다는 것을 알 수 있다. 동시에, 또한 막 균일도와 같은 특성을 개선하기 위하여 웨이퍼 표면에 따른 모든 위치에 대한 처리 가스의 운반을 정확히 제어하는 방법을 제공하는 것이 바람직하다. 이미 개시된 바와 같이, 막 증착 균일도를 개선하는데 사용된 한가지 방법은 미국 특허 출원 제08/571,618호에 개시되어 있다. 이런 개선에도 불구하고, 상기 관련 목적을 달성하기 위한 새로운 기술들이 최근의 과학 기술과 보조를 맞추기 위해 지속적으로 연구되고 있다.As mentioned above, it can be seen that it is desirable to produce an oxide film having a reduced dielectric constant, such as an FSG film. At the same time, it is also desirable to provide a method for precisely controlling the delivery of processing gas to all locations along the wafer surface in order to improve properties such as film uniformity. As already disclosed, one method used to improve film deposition uniformity is disclosed in US patent application Ser. No. 08 / 571,618. In spite of these improvements, new techniques for achieving these related objectives are constantly being researched to keep pace with recent scientific techniques.
본 발명의 목적은 개선된 가스 운반 시스템을 결합한 개선된 증착 챔버 및 낮은 유전 상수와 개선된 균일도를 가지는 막을 증착하는 방법을 제공하는 것이다.It is an object of the present invention to provide an improved deposition chamber incorporating an improved gas delivery system and a method for depositing films having low dielectric constants and improved uniformity.
도 1은 종래 기술의 특징적 M형 증착 두께 변화 플롯을 도시하는 과장도. 도 2는 미국 특허 출원 제 08/571,618호의 장치를 사용한 도 1의 증착 두께 변화의 개선을 도시하는 도면.1 is an exaggerated diagram showing a characteristic M-type deposition thickness variation plot of the prior art. FIG. 2 shows an improvement of the deposition thickness change of FIG. 1 using the apparatus of US patent application 08 / 571,618.
도 3은 본 발명의 일실시예에 따라 제조된 증착 챔버를 도시하는 개략적 단면도.3 is a schematic cross-sectional view illustrating a deposition chamber made in accordance with one embodiment of the present invention.
도 4는 SiF4대 실란의 서로 다른 흐름 속도비에 대한 유전 상수 대 산소 흐름의 그래프.4 is a graph of dielectric constant versus oxygen flow for different flow rate ratios of SiF 4 to silane.
도 5는 3개 구멍을 가지는 도 3의 중앙 노즐에 대한 다른 실시예의 개략도.5 is a schematic representation of another embodiment of the central nozzle of FIG. 3 with three holes;
도 6은 부가적 산소 통로를 도시하는 중앙 노즐의 영역도.6 is an area view of a central nozzle showing additional oxygen passages.
* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings
34, 34a : 노즐 38 : 구멍34, 34a: nozzle 38: hole
56 : 중앙 노즐 70 : 가스 통로56 center nozzle 70 gas passage
76 : 환형 구멍 78 : 유체 시일76: annular hole 78: fluid seal
본 발명은 개선된 가스 운반 시스템을 결합한 개선된 증착 챔버의 제공에 관한 것이다. 상기 가스 운반 시스템은 적당한 비율의 처리 가스가 웨이퍼 표면에 걸쳐 균일하게 운반되도록 한다. 또한 본 발명은 낮은 유전 상수와 개선된 균일도를 가지는 FSG막을 증착하는 방법에 관한 것이다. 이것은 (1) 기판에 대한 가스(바람직하게 실란, SiF4또는 CF4와 같은 플로오르 공급용 가스, 및 O2또는 N20과 같은 산소 공급용 가스)의 적용, (2) 바람직하게 특별한 챔버를 사용하여 테스트 결과로서 결정되어지는 상기 가스의 최적 흐름 속도 선택의 조합에 의해 달성된다. 일부 실시예에서, 도핑된 FSG막은 3.4 또는 3.3 만큼 낮은 유전 상수를 가진다. 바람직하게, 상기 FSG막의 유전 상수는 적어도 3.5 이하이다.The present invention relates to the provision of an improved deposition chamber incorporating an improved gas delivery system. The gas delivery system ensures that an appropriate proportion of process gas is uniformly transported across the wafer surface. The invention also relates to a method for depositing an FSG film having a low dielectric constant and improved uniformity. This includes (1) application of a gas to the substrate (preferably silane, a gas for flow supply such as SiF 4 or CF 4 , and an oxygen supply gas such as O 2 or N 2 0), (2) preferably a special chamber By means of a combination of the optimum flow rate selection of the gas, which is determined as a test result. In some embodiments, the doped FSG film has a dielectric constant as low as 3.4 or 3.3. Preferably, the dielectric constant of the FSG film is at least 3.5 or less.
개선된 증착 챔버는 증착 챔버를 한정하는 하우징을 포함한다. 기판 지지대는 증착 챔버내에 하우징된다. 제 1 가스 분배기는 기판 지지용 표면으로부터 일정 간격 배치되고 일반적으로 기판 지지용 표면의 주변 둘레에 중첩하는 주변 패턴내에 있는 증착 챔버내로 개방되는 구멍 또는 다른 출구를 가진다. 기판 지지용 표면으로부터 그 위에 일정 간격 배치되는 제 2 가스 분배기, 바람직하게 중앙 노즐이 사용되며, 제 3 가스 분배기가 기판 상에 중심적인 영역에서 하우징 상부를 통해 챔버로 산소 공급용 가스(예를 들면, O2)를 운반한다. 이것은 바람직하게 실란(그리고 다른 가스)을 운반하는 중앙 노즐과 하우징의 상부에 있는 홀 사이에 형성된 환형 구멍을 통해 산소를 통과시킴으로써 달성된다. 일실시예에서 제 1 가스 분배기는 제 1 및 제 2 노즐 세트를 포함한다.The improved deposition chamber includes a housing defining a deposition chamber. The substrate support is housed in the deposition chamber. The first gas distributor has holes or other outlets that are spaced from the substrate support surface and open into the deposition chamber that are generally in a peripheral pattern that overlaps around the periphery of the substrate support surface. A second gas distributor, preferably a central nozzle, is used which is spaced above it from the substrate support surface, and wherein the third gas distributor is used for supplying oxygen (e. G. , O 2 ). This is preferably accomplished by passing oxygen through an annular hole formed between a central nozzle carrying silane (and other gases) and a hole in the top of the housing. In one embodiment the first gas distributor comprises a first and a second nozzle set.
본 발명의 일실시예에서, FSG 막은 실란, 산소 및 SiF4를 포함하는 처리 가스로부터 증착된다. 산소와 SiF4는 제 1 노즐 세트를 통해 챔버로 함께 운반되고, 실란(또는 실란과 SiF4)은 제 2 노즐 세트를 통해 운반된다. 산소와 SiF4의 혼합 및 제 1 노즐 세트를 통한 이런 혼합물의 유입은 장비 복잡성을 감소시켜 비용이 감소될 수 있다. 또한 실란(또는 실란과 SiF4)은 제 2 가스 분배기의 사용없이 달성되는 기판 상부에 대한 가스의 균일한 적용을 개선하기 위해 제 2 가스 분배기로부터 진공 챔버내로 주입되고, 산소는 제 3 가스 분배기를 통해 운반된다. 이런 식으로, 산소는 바람직하게 SiF4와 함께 제 1 가스 분배기의 제 1 노즐 세트를 통해 측면으로부터, 또한 기판 상의 실란과 같이 동일 영역내로 공급된다. 또한, 환형 구멍을 통한 산소의 통로는 챔버내의 반응 가스가 하우징의 상부와 중앙 노즐이 연장하는 몸체 사이에 사용된 시일의 손상을 방지한다. 이런 장점은 실란이 환형 노즐을 통해 통과하고 산소가 중앙 노즐을 통해 통과한다면 계속 유지된다.In one embodiment of the present invention, the FSG film is deposited from a processing gas comprising silane, oxygen and SiF 4 . Oxygen and SiF 4 are carried together through the first nozzle set to the chamber, and silane (or silane and SiF 4 ) is carried through the second nozzle set. Mixing oxygen and SiF 4 and introducing this mixture through the first nozzle set can reduce equipment complexity and reduce costs. Silane (or silane and SiF 4 ) is also injected from the second gas distributor into the vacuum chamber to improve uniform application of gas to the substrate top, which is achieved without the use of a second gas distributor, and oxygen is injected into the third gas distributor. Is carried through. In this way, oxygen is preferably supplied together with SiF 4 from the side through the first set of nozzles of the first gas distributor and into the same region as the silane on the substrate. In addition, the passage of oxygen through the annular aperture prevents damage of the seal in which the reactive gas in the chamber is used between the top of the housing and the body from which the central nozzle extends. This advantage persists if silane passes through the annular nozzle and oxygen passes through the central nozzle.
또한 막 두께와 유전 상수 균일도는 기판의 온도가 기판에 걸쳐 균일하게 유지되는 것을 보장하고 스퍼터링 균일도를 달성하도록 디자인된 소스 RF 발생기를 사용함으로써 증진된다.Film thickness and dielectric constant uniformity are also enhanced by using a source RF generator designed to ensure that the temperature of the substrate remains uniform across the substrate and to achieve sputtering uniformity.
본 발명의 주요 특징 중 하나는 챔버에 진입하는 산소의 균일한 분배를 보장하는 것이 매우 중요하다고 하는 인식이다. 이것은 챔버의 상부와 챔버의 측면으로부터 산소를 흘려줌으로써 달성된다. 부가적으로, 챔버의 상부를 통한 산소 흐름 경로의 적당한 구성에 의해, 산소는 플루오르와 같은 반응 가스와의 접촉에서 발생하는 유해한 현상으로부터 시일링 엘리먼트를 보호하도록 소용될 수 있다.One of the main features of the present invention is the recognition that it is very important to ensure a uniform distribution of oxygen entering the chamber. This is accomplished by flowing oxygen from the top of the chamber and from the side of the chamber. In addition, by proper configuration of the oxygen flow path through the top of the chamber, oxygen can be used to protect the sealing element from harmful phenomena that occur in contact with the reactant gas, such as fluorine.
기판에 균일하게 가스를 공급하는 필요에 부가적으로, 안정된 막을 증착하고 막에 대한 최소 유전 상수를 달성하기 위하여 O2, SiH4및 SiF4와 같은 가스의 정확한 비율을 사용하는 것이 필요하다. 각각에 대한 적당한 흐름 속도는 사용된 특정 챔버에 따라 다를 것이다. 따라서, 최소 유전 상수를 갖는 고밀도 유전체 막을 제공하는 다양한 흐름 속도 비율을 테스트하는 것이 본 발명의 다른 특징이다.In addition to the need to supply gas evenly to the substrate, it is necessary to use the correct proportions of gases such as O 2 , SiH 4 and SiF 4 to deposit stable films and achieve minimum dielectric constants for the films. The appropriate flow rate for each will depend on the specific chamber used. Thus, it is another feature of the present invention to test various flow rate ratios that provide high density dielectric films with a minimum dielectric constant.
본 발명의 다른 특징과 장점은 바람직한 실시예가 첨부된 도면과 관련하여 상세히 설명되는 다음의 상세한 설명으로부터 도출될 것이다.Other features and advantages of the invention will be derived from the following detailed description in which preferred embodiments are described in detail in conjunction with the accompanying drawings.
도 3은 2개 세트의 RF 유도 코일(8, 9)에 의해 둘러싸여진 일반적으로 실린더화된 유전체 밀폐체(6)를 구비하는 하우징(4)을 포함하는 증착 챔버(2)를 설명한다. 밀폐체(6)는 유전체 재료 외에 RF 투명 재료로 제조될 수 있다. 코일(8, 9)은 한쌍의 소스 RF 발생기(10, 11)에 의해 전력이 공급된다. 또한 챔버(2)는 하우징(4)내에 한정된 상기 진공 챔버(18)내에 기판 지지용 표면(16)을 가지는 수냉식 기판 지지대(14)를 포함한다. 표면(16)은 챔버(18)내에서 기판(20)을 지지하는데 사용된다. 기판 지지대(14)는 캐소드로서 기능하고 정합 회로(24)를 통해 바이어스 RF 발생기(22)에 접속된다. 하우징(4)의 일반적으로 실린더형 측벽(30)은 하우징(4)의 하부(32)를 유전체 밀폐체(6)에 접속시킨다. 측벽(30)은 애노드로서 기능한다.FIG. 3 illustrates a deposition chamber 2 comprising a housing 4 having a generally cylinderized dielectric enclosure 6 surrounded by two sets of RF induction coils 8, 9. The seal 6 can be made of an RF transparent material in addition to the dielectric material. The coils 8, 9 are powered by a pair of source RF generators 10, 11. The chamber 2 also includes a water cooled substrate support 14 having a substrate support surface 16 in the vacuum chamber 18 defined in the housing 4. Surface 16 is used to support substrate 20 in chamber 18. The substrate support 14 functions as a cathode and is connected to the bias RF generator 22 through a matching circuit 24. The generally cylindrical sidewall 30 of the housing 4 connects the lower portion 32 of the housing 4 to the dielectric enclosure 6. Side wall 30 functions as an anode.
처리 가스는 균등하게 일정 간격 배치된 2개 세트의 12개 노즐(34, 34a)을 통해 기판(20)을 둘러싸는 영역에서 진공 챔버(18)로 유입된다. 노즐(34, 34a)은 링형 패턴으로 배열되고 각각 가스 매니폴드(36, 36a)에 유동적으로 결합된다. 매니폴드(36, 36a)는 제 1 및 제 2 가스 소스(35, 35a)로부터 제 1 및 제 2 가스 제어기(33, 37a)와 제 1 및 제 2 가스 공급 라인(39, 39a)을 통해 처리 가스를 공급한다. 각각의 노즐(34, 34a)은 그것의 말단부에 구멍(38)을 가진다. 상기 노즐(34, 34a)의 구멍(38)은 기판 지지대(14)의 주변 상에 배열되고 그러므로 기판(20)의 주변(42) 상에 배열된다. 진공 챔버(18)는 배기 포트(44)를 통해 배기된다.The processing gas enters the vacuum chamber 18 in a region surrounding the substrate 20 through two sets of twelve nozzles 34, 34a evenly spaced apart. The nozzles 34, 34a are arranged in a ring pattern and are fluidly coupled to the gas manifolds 36, 36a, respectively. Manifolds 36 and 36a are processed from first and second gas sources 35 and 35a through first and second gas controllers 33 and 37a and first and second gas supply lines 39 and 39a. Supply gas. Each nozzle 34, 34a has a hole 38 at its distal end. The holes 38 of the nozzles 34, 34a are arranged on the periphery of the substrate support 14 and are therefore arranged on the perimeter 42 of the substrate 20. The vacuum chamber 18 is exhausted through the exhaust port 44.
상기 챔버(2)의 여러 가지 컴포넌트는 처리기(도시 안됨)에 의해 제어된다. 상기 처리기는 컴퓨터 판독 가능 매체(또한 도시 안됨)의 제어하에 동작한다. 상기 컴퓨터 프로그램은 여러 가지 동작 파라미터, 이를테면 시간, 가스의 혼합, 챔버 압력, 기판 지지 온도 및 RF 전력 레벨을 명령한다.Various components of the chamber 2 are controlled by a processor (not shown). The processor operates under the control of a computer readable medium (also not shown). The computer program commands various operating parameters, such as time, mixing of gases, chamber pressure, substrate support temperature and RF power level.
본 발명은 기판 상에 배치된 개선된 가스 운반 컴포넌트(65)를 제공함으로써 이미 개시된 구조에서 개선된다. 바람직한 실시예에서, 가스 운반 컴포넌트(65)는 밀폐체(6)의 상부에 장착된 몸체(72)내에 형성된 가스 통로(70)를 포함한다. 중앙 노즐(56)이 상부(75)에 형성된 개구부(74)를 통과한다. 노즐(56)과 개구부(74)는 진공 챔버(18)와 가스 통로(70)와 유체 연통하는 환형 구멍(76)을 제공한다. 유체 시일(78)이 몸체(72)와 상부(75) 사이에 제공된다. 그러므로 가스는 통로(70)를 통해, 유체 시일(78)에 의해 구속되며, 최종적으로 환형 구멍(76)을 따라 몸체(72)와 상부(75) 사이에 한정된 영역내로 진행한다.The present invention is improved in the structure already disclosed by providing an improved gas delivery component 65 disposed on a substrate. In a preferred embodiment, the gas delivery component 65 comprises a gas passage 70 formed in a body 72 mounted on top of the closure 6. The central nozzle 56 passes through the opening 74 formed in the upper portion 75. The nozzle 56 and the opening 74 provide an annular hole 76 in fluid communication with the vacuum chamber 18 and the gas passage 70. A fluid seal 78 is provided between the body 72 and the top 75. The gas is therefore constrained by the fluid seal 78 through the passage 70 and finally progresses along the annular hole 76 into the area defined between the body 72 and the top 75.
바람직한 실시예에서, 본 발명의 장치는 실란, 산소 및 SiF4선구물질 가스로부터 FSG 막을 증착하는데 사용된다. 이런 실시예에서, 본 발명은 바람직하게 제 1 가스 소스(35)로부터 SiF4와 산소의 혼합물을 노즐(34)의 구멍(38)을 통해 챔버(18)내로 유입한다. 이렇게 하여 가스 운반을 단순화함으로써 비용 절감을 가져온다. 실란(SiH4)은 바람직하게 제 2 가스 소스(35a)로부터 제 2 가스 제어기(37a)와 노즐(34a)을 통해 챔버(18)내로 운반된다. 부가적으로, 제 3 가스 소스(58)는 바람직하게 상기 기판(20)으로부터 챔버(18)내로 실란(또는 실란과 SiF4의 혼합물)을 유입하는데 사용된다. 이와 관련하여, 또한 산소는 기판(20) 상부의 위치로부터 통로(70)와 환형 구멍(76)을 통해 실란의 흐름 경로와 분리된 흐름 경로를 따라 챔버(18)내로 향하게 된다.In a preferred embodiment, the apparatus of the present invention is used to deposit FSG films from silane, oxygen and SiF 4 precursor gases. In this embodiment, the present invention preferably introduces a mixture of SiF 4 and oxygen from the first gas source 35 into the chamber 18 through the aperture 38 of the nozzle 34. This leads to cost savings by simplifying gas delivery. Silane SiH 4 is preferably conveyed from the second gas source 35a into the chamber 18 through the second gas controller 37a and the nozzle 34a. In addition, a third gas source 58 is preferably used to introduce silane (or a mixture of silane and SiF 4 ) from the substrate 20 into the chamber 18. In this regard, oxygen is also directed from the position above the substrate 20 through the passage 70 and the annular aperture 76 into the chamber 18 along a flow path separate from the flow path of the silane.
산소는 상대적으로 안정한 가스, 이를테면 SiF4와 혼합될 수 있다. 그러나, 실란과 산소의 반응 특성 때문에 이런 성분들은 이들의 챔버(18)내로의 유입때까지 개별적으로 유지되어야 한다. 이것을 달성하기 위하여, 개별 노즐(34, 34a)이 기판 지지대(14) 둘레의 영역에 사용된다. 또한 산소가 몸체(72)에 형성된 가스 통로(70)를 통해 유입된다. 이런 식으로 산소를 주입함으로써, 마찬가지로 유체 시일(78)에 대한 유해한 현상을 가질 수 있는 플루오르 성분과 같은 가스가 산소 흐름의 세정 현상 또는 세척 현상에 의해 유체 시일에 도달하지 못하도록 한다. 다른 실시예에서, 또한 시일(78)이 열화되지 않도록 하는 산소외의 가스가 사용될 수 있다.Oxygen can be mixed with a relatively stable gas, such as SiF 4 . However, due to the reaction properties of silane and oxygen, these components must be maintained individually until their entry into the chamber 18. To achieve this, individual nozzles 34 and 34a are used in the area around the substrate support 14. Oxygen is also introduced through the gas passage 70 formed in the body 72. By injecting oxygen in this way, gases such as fluorine components, which may likewise have a deleterious effect on the fluid seal 78, are prevented from reaching the fluid seal by a cleaning phenomenon or a cleaning phenomenon of the oxygen flow. In other embodiments, gases other than oxygen may also be used to prevent the seal 78 from deteriorating.
가스 통로(70)를 통해 산소를 운반하는 다른 장점은 산소가 실란 또는 일부 다른 가스와 비교할 때 상대적으로 긴 체류 시간을 가진다는 것이다. 실란의 짧은 체류 시간 때문에, 실란이 구멍(76)을 통해 유입될 때 상대적으로 빨리 분해될 수 있어 구멍내에 미립자를 형성하고 통로(70)에 있는 구멍의 업스트림을 초래한다. 분자 산소는 실란보다 더 긴 체류 시간을 가지고, 그러므로 대신에 산소가 구멍(76)을 통해 운반될 때 문제가 발생하지 않는다.Another advantage of transporting oxygen through the gas passage 70 is that the oxygen has a relatively long residence time when compared to silane or some other gas. Because of the short residence time of the silane, the silane can decompose relatively quickly as it enters through the hole 76, forming particulates in the hole and causing upstream of the hole in the passage 70. Molecular oxygen has a longer residence time than silane and therefore no problem occurs when oxygen is transported through the hole 76 instead.
이런 방식의 FSG 막의 증착은 3.5 미만, 및 3.4 또는 3.3 이하 조차의 유전 상수를 가지는 안정한 막(450℃까지의 온도에서 HF 또는 H2O 가스 방출이 없는)을 초래한다. 이런 낮은 유전 상수값은 기판(20)에 걸쳐 일반적으로 균일한 방식으로 달성된다. 유전 상수의 균일한 감소는 소자 크기가 감소되고 가깝게 배치된 도체 사이의 캐패시턴스가 자연적으로 증가할 것이기 때문에 중요하다. 캐패시턴스를 감소하여 소자의 동작 속도를 증가하기 위해, 증착된 유전체 막의 유전 상수는 감소되어야 한다.Deposition of FSG films in this manner results in stable films (without HF or H 2 O gas release at temperatures up to 450 ° C.) with dielectric constants below 3.5, and even below 3.4 or 3.3. This low dielectric constant value is achieved in a generally uniform manner across the substrate 20. Uniform reduction in dielectric constant is important because device size is reduced and capacitance between closely spaced conductors will naturally increase. In order to reduce capacitance and increase the device's operating speed, the dielectric constant of the deposited dielectric film must be reduced.
이미 기술된 상기 구조를 사용하는 가스 분배의 균일도와 관련하여, 균일한 유전 상수는 또한 기판(20)에 걸친 온도 균일도와 스퍼터링 균일도에 의존한다. 예를 들면, 기판에 따른 더욱 균일한 온도 분배를 달성하는데 사용될 수 있는 구조의 설명을 위해 1996년 4월 25일에 제출되고 감소된 접촉 면적과 온도 피드백을 가지는 압력대를 갖는 기판 지지대로 명명되고 어플라이드 머티어리얼스, 인코포레이티드에 양도된 미국 특허 출원 제 08/641,147호를 참조하라. 1995년 2월 15일에 제출되고 유도 결합된 플라즈마 반응기의 RF 전력 소스에 대한 자동 주파수 튜닝으로 명명된 미국 특허 제08/389,888호와 1995년 7월 26에 제출되고 전기적 가변 밀도 프로파일을 가진 플라즈마 소스로 명명되고 또한 어플라이드 머티어리얼스, 인코포레이티드에 양도된 미국 특허 출원 제08/507,726호는 증진된 스퍼터링 균일도를 위한 구조를 개시하고 있다.Regarding the uniformity of gas distribution using the above described structure, the uniform dielectric constant also depends on the temperature uniformity and the sputtering uniformity across the substrate 20. For example, filed on April 25, 1996 for the description of a structure that can be used to achieve a more uniform temperature distribution along the substrate and named as a substrate support having a pressure zone with reduced contact area and temperature feedback. See US patent application Ser. No. 08 / 641,147, assigned to Applied Materials, Inc. US Patent No. 08 / 389,888, filed Feb. 15, 1995 and named Automatic Frequency Tuning for RF Power Sources of Inductively Coupled Plasma Reactors, and Plasma Sources with Electrically Variable Density Profiles, filed on July 26, 1995 US Patent Application No. 08 / 507,726, also assigned to Applied Materials, Inc., discloses a structure for enhanced sputtering uniformity.
SiF4와 실란의 전체 흐름의 변화는 증착 속도와 처리량에 영향을 끼친다. 높은 처리량은 높은 스퍼터링과 높은 에칭 속도를 형성하도록 바이어스 전력 소스(22)로부터 높은 바이어스 전력을 요구한다. 에칭 속도는 기판의 온도에 의해 강하게 영향을 받기 때문에 높은 바이어스 전력과 높은 처리량은 기판(20)에 걸친 온도 균일도가 달성되는 경우에만 가능하다.Changes in the overall flow of SiF 4 and silane affect the deposition rate and throughput. High throughput requires high bias power from bias power source 22 to form high sputtering and high etch rate. Since the etch rate is strongly influenced by the temperature of the substrate, high bias power and high throughput are only possible if temperature uniformity across the substrate 20 is achieved.
사용될 상기 SiF4, 실란(SiH4)과 산소의 양의 결정은 전체 새로운 층의 복잡성을 형성한다. 실리콘(예를 들어 SiH4와 SiF4)의 흐름 속도가 일정하게 유지한다고 가정하면, 수개의 기본적인 보고서가 이런 여러 가지 구성의 사용을 고려하여 형성될 수 있다고 믿어진다. 너무 적은 산소가 사용된다면, 상기 증착 속도는 극도로 떨어져 너무 비능률적인 처리를 형성한다. 너무 적은 산소는 상기 막에 편입된 과잉 플루오르를 가진 실리콘이 풍부한 막을 남길 수 있다. 너무 많은 산소가 사용된다면, 얻어지는 막은 더많은 USG가 되고 상기 유전 상수는 높아진다. 너무 많은 SiF4가 사용된다면, 노화 문제를 초래할 수 있고, 노화 문제는 시간에 걸쳐 플루오르가 상기 얻어지는 막의 복잡한 화학적 작용 상태에서 단단히 결합되지 않고 방출되기 때문에 초래되고 소자의 열화를 초래한다. 너무 많은 실란은 상기 막이 더욱 USG 처럼 행동하도록 할 것이고 그러므로 바람직하지 않은 레벨의 유전 상수를 초래한다.The determination of the amount of SiF 4 , silane (SiH 4 ) and oxygen to be used forms the complexity of the whole new layer. Assuming that the flow rates of silicon (eg SiH 4 and SiF 4 ) remain constant, it is believed that several basic reports can be formed considering the use of these different configurations. If too little oxygen is used, the deposition rate is extremely low, forming too inefficient treatment. Too little oxygen can leave a silicon rich film with excess fluorine incorporated into the film. If too much oxygen is used, the resulting film becomes more USG and the dielectric constant becomes higher. If too much SiF 4 is used, it can lead to aging problems, which are caused over time because fluorine is released without being tightly bound in the complex chemical state of the resulting film and leads to degradation of the device. Too much silane will cause the membrane to behave more like USG and therefore lead to undesirable levels of dielectric constant.
상기 기판 표면에서 산소, SiF4및 실란의 광학적 양은 화학량론적 비율이다. 그러나, 챔버(2)와 다른 증착 챔버를 포함하는 증착 챔버내의 흐르는 가스의 화학량론적 비율은 상기 화학량론적 비율이 아닌 기판 표면에서의 가스 비율을 초래할 것이다. 상기 기판 표면에서의 화학량론적 비율을 달성하는데 요구되는 상기 증착 챔버내로 흐르는 가스의 실제 비율은 특정 챔버의 구조에 따라 적어도 부분적으로 상기 화학량론적 비율으로부터 변화할 것이다. 상기 챔버에 더욱 효과적이고, 화학량론적 양에 더 가까운 가스 흐름 속도가 사용될 수 있도록 가스는 적게 낭비된다.The optical amounts of oxygen, SiF 4 and silane at the substrate surface are in stoichiometric proportions. However, the stoichiometric ratio of the flowing gas in the deposition chamber, including chamber 2 and other deposition chambers, will result in a gas ratio at the substrate surface that is not the stoichiometric ratio. The actual proportion of gas flowing into the deposition chamber required to achieve the stoichiometric ratio at the substrate surface will vary from the stoichiometric ratio at least in part depending on the structure of the particular chamber. Less gas is wasted so that a gas flow rate that is more effective for the chamber and closer to stoichiometric amounts can be used.
3.5 이하, 바람직하게 3.4 이하 및 더욱 바람직하게 3.3 이하의 바람직한 유전 상수를 달성하도록 특별한 챔버에 대한 SiF4, 실란 및 산소의 적당한 관련 흐름 속도를 결정하기 위하여, 3개 성분의 비율은 기판(20)상에 다수의 유전체막을 형성하도록 어떤 요구된 방식으로 변경될 수 있다. 다음에 각각의 유전체막에 따른 서로 다른 위치에서의 유전 상수가 측정될 수 있다. 그러나, 일부는 정리되어 있는 관련 양으로 제한된다. SiF4의 비율은 너무 많거나 너무 적은 SiF4와 실란을 초래하는 문제를 감소하거나 제거하도록 전체 실리콘 공급용 가스의 약 40% 내지 60%가 되어야 한다. 산소는 전체 실리콘 공급용 가스의 약 60% 내지 100% 사이가 될 것이다.In order to determine the appropriate relative flow rates of SiF 4 , silane and oxygen for a particular chamber to achieve a desired dielectric constant of 3.5 or less, preferably 3.4 or less and more preferably 3.3 or less, the ratio of the three components is determined by the substrate 20. It can be altered in any desired manner to form multiple dielectric films on it. The dielectric constants at different locations along each dielectric film can then be measured. However, some are limited to the relevant amounts that are listed. Ratio of SiF 4 should be approximately 40% to 60% of total silicon fed gas so as to reduce or eliminate the problems that result in too much or too little SiF 4 and silane. Oxygen will be between about 60% and 100% of the total silicon feed gas.
도 4는 SiF4: 실란 : 산소의 비율을 변경하여 실행된 테스트 세트의 결과를 도시한다. 전체 반응 가스 흐름 속도(일정한 양의 실란으로 초래하는), 즉 SiF4와 실란의 조합을 위한 흐름 속도, 즉 SiF4와 실란의 화합물에 대한 흐름 속도(일정한 양의 실리콘을 초래하는)를 선택하고, SiF4와 실란의 여러 가지 비율을 얻기 위하여 SiF4와 실란 사이의 합계를 분할하고 다음에 이런 비율을 사용하여 산소 흐름을 변화시킴으로써, 유전 상수 대 산소 흐름의 도 4에 도시된 그래프가 형성된다. 이런 형태의 그래프는 매우 유용한 데이터를 제공한다.4 shows the results of a test set performed by varying the ratio of SiF 4 : silane: oxygen. Select the whole reaction gas flow rates (which results in a certain amount of the silane), that is, SiF 4 and the flow rate for the combination of the silane, that is, SiF 4 and (resulting in the amount of silicon constant) flow rate for the compounds of the silane and , by dividing the sum between SiF 4 and silane in order to obtain a number of the ratio of SiF 4 and the silane and varying the oxygen flow using this rate in the following, the dielectric constant for the oxygen flow is formed in the graph shown in Figure 4 . This type of graph provides very useful data.
44 sccm SiF4대 36.4 sccm 실란으로부터 초래하는 플롯 A는 약 62 sccm의 산소 흐름에서 3.4로부터 약 110 sccm의 산소 흐름 속도에서 약 3.8까지 변화하는 유전 상수를 초래한다. 상기 최소 유전 상수가 SiF4대 실란의 이런 비율을 위한 것이라는 것에 대해서는 상기 그래프로부터 명확하지 않다. 그러나, 최소값은 부적절하게 낮은 산소 흐름 속도에서 발생한다는 것을 나타낸다. 36 대 44.4의 SiF4대 실란의 sccm 흐름 속도비를 가지는 플롯 B는 최저 유전 상수, 즉 60 sccm의 산소 흐름에서 약 3.2를 제공한다. 플롯 C와 D는 각각 약 3.5와 3.6의 최소 유전 상수를 가진다. 이런 그래프로부터 특별한 비율의 SiF4대 실란에 대해, 플롯 B에 대한 비율은 수용할 수 있는 레벨에 있는 산소 흐름으로 최저 유전 상수를 제공한다는 것을 알 수 있다. 플롯 A와 B의 검토는 이런 2개 플롯에 대한 특성 사이의 SiF4대 실란의 특성이 플롯 B에 대한 특성으로 달성할 수 있는 것보다 더 낮은 유전 상수를 산출할 수 있다는 것을 제시한다.Plot A resulting from 44 sccm SiF 4 vs. 36.4 sccm silane results in a dielectric constant that varies from 3.4 to about 3.8 at an oxygen flow rate of about 110 sccm at an oxygen flow of about 62 sccm. It is not clear from the graph that the minimum dielectric constant is for this ratio of SiF 4 to silane. However, the minimum value indicates that it occurs at an inappropriately low oxygen flow rate. Plot B with a sccm flow rate ratio of 36 to 44.4 SiF 4 to silane gives the lowest dielectric constant, about 3.2, at an oxygen flow of 60 sccm. Plots C and D have minimum dielectric constants of about 3.5 and 3.6, respectively. From this graph it can be seen that for a particular ratio of SiF 4 to silane, the ratio for plot B gives the lowest dielectric constant with oxygen flow at an acceptable level. A review of plots A and B suggests that the properties of SiF 4 versus silane between the properties for these two plots can yield lower dielectric constants than can be achieved with properties for plot B.
따라서, 본 발명은 감소된 유전 상수를 달성하도록 SiF4(또는 다른 플루오르 공급용 가스)와 실란 화학을 사용하여 낮은 유전 상수를 가진 막을 달성하는 방법을 결정하는 유용하고 효과적인 방법을 제공한다. 각각의 테스트에 대한 단일 합계 반응 가스 흐름 속도를 선택하기 위해 이미 기술된 방법이 현재 채용되지만, 유전 상수 정보의 정돈된 수집을 위한 다른 방법이 또한 추구될 수 있다. 예를 들면, 모든 3개 변수가 전체 파라미터내에서 변화될 것이 요구될 수 있다.Accordingly, the present invention provides a useful and effective method of determining how to achieve films with low dielectric constants using SiF 4 (or other fluorine supply gas) and silane chemistry to achieve reduced dielectric constants. While the methods previously described are currently employed to select a single sum reaction gas flow rate for each test, other methods for orderly collection of dielectric constant information can also be pursued. For example, all three variables may be required to be changed within the overall parameter.
사용중에, 낮은 유전 상수를 가지는 막은 우선 전형적으로 서로 다른 테스트 결과를 플롯팅함으로써 이미 개시된 방법으로 상기 SiF4, 실란 및 산소의 적당한 흐름 속도를 결정함으로써 기판(20) 상에 증착될 수 있다. 특별한 챔버에 대한 요구 속도가 결정될 때, 실란은 제 2 가스 소스(35a)로부터 챔버(18)내로 유입되고, 실란과 SiF4의 혼합물은 제 3 가스 소스(58)로부터 챔버내로 유입되고, 산소는 산소 소스(71)로부터 상기 챔버내로 유입되며, 산소와 SiF4의 혼합물은 제 1 가스 소스(35)로부터 챔버(18)내로 유입된다. 또한 아르곤은 제 1 및 제 3 소스(35, 58)로부터 유입된다. 또한 증착 균일도는 기판(20)의 온도가 기판 표면 상에서 균일하게 제어되도록 보장함으로써, 그리고 균일한 스퍼터링의 달성을 보조하는 가변 주파수 소스 RF 발생기(10, 11)의 사용에 의해 보조된다.In use, a film having a low dielectric constant can be deposited on the substrate 20 by first determining the proper flow rate of the SiF 4 , silane and oxygen in the already disclosed method, typically by plotting different test results. When the required rate for a particular chamber is determined, silane enters the chamber 18 from the second gas source 35a, a mixture of silane and SiF 4 flows into the chamber from the third gas source 58, and oxygen From the oxygen source 71 is introduced into the chamber, a mixture of oxygen and SiF 4 is introduced from the first gas source 35 into the chamber 18. Argon also flows in from the first and third sources 35, 58. Deposition uniformity is also assisted by ensuring that the temperature of the substrate 20 is uniformly controlled on the substrate surface, and by the use of variable frequency source RF generators 10 and 11 to assist in achieving uniform sputtering.
이미 기술된 실시예는 8인치(20 ㎝)의 직경을 가지는 기판(20)을 위해 디자인된다. 더 큰 직경의 기판, 이를테면 12 인치(30 ㎝)의 직경을 가지는 기판은 상기 노즐 장치(56')에 의해 도 5에 도시된 바와 같은 다중 중앙 노즐(56a)의 사용을 요구할 수 있다. 이런 실시예에서 상기 증착 두께 변화 플롯은 아마 3개 범프(도 3에 도시된 바와 같은), 4개 범프 또는 5개 범프 모양을 가질 것이다. 상기 증착 두께 플롯에 대한 특별한 모양은 중앙 노즐(54A)과 구멍(64)의 형태, 수, 방향 및 간격에 의해 영향을 받게 될 것이다.The embodiment already described is designed for a substrate 20 having a diameter of 8 inches (20 cm). Larger diameter substrates, such as substrates having a diameter of 12 inches (30 cm), may require the use of multiple central nozzles 56a as shown in FIG. 5 by the nozzle arrangement 56 '. In this embodiment the deposition thickness change plot will probably have three bumps (as shown in FIG. 3), four bumps or five bump shapes. The particular shape for the deposition thickness plot will be affected by the shape, number, direction and spacing of the central nozzle 54A and the aperture 64.
구멍(76)에 부가적으로, 또한 산소는 도 6에 도시된 바와 같은 다수의 하향 및 외부로 연장하는 통로(80)를 통해 챔버(18)내로 진입될 수 있다. 각각의 통로(80)는 산소가 챔버(18)내로 진입하는 구멍(82)을 가진다. 필요하다면, 다른 가스, 이를테면 아르곤은 구멍(64)을 통과하는 실란 또는 환형 구멍(76) 또는 구멍(82)을 통과하는 산소 중 하나 또는 둘다와 혼합될 수 있다.In addition to the aperture 76, oxygen may also enter the chamber 18 through a number of downward and outwardly extending passageways 80 as shown in FIG. 6. Each passage 80 has a hole 82 through which oxygen enters the chamber 18. If desired, other gases, such as argon, may be mixed with one or both of silane passing through the holes 64 or annular holes 76 or oxygen passing through the holes 82.
변형 및 변화가 다음의 청구범위에 한정된 바와 같은 본 발명의 주제를 벗어나지 않고 개시된 실시예로 만들어질 수 있다. 예를 들면, 중앙 노즐(56)은 다중 출구 또는 가스 출구의 원형 어레이를 가지는 가스 분배기의 샤워 헤드 형태에 의해 대체될 수 있다. 유사하게, 노즐(34, 34a 또는 56a)은 처리 가스가 챔버(18)내로 운반되는 가스 출구 또는 구멍을 가지는 링 또는 링형 구조물에 의해 대체될 수 있다. 개별적 노즐(34, 34a)이 바람직하더라도, 단일 세트의 노즐(34)이 산소가 아닌 실란과 SiF4를 공급하는데 사용될 수 있다. 구멍(76)은 환형 링이라기 보다 중앙 노즐(56) 근처에 원형 형태로 배열된 다수의 작은 개구를 포함할 수 있다. 또한, 산소 소스(71)와 제 3 가스 소스(58)는 소스(71)가 노즐(56)에 연결되고 소스(58)가 통로(70)에 연결되도록 전환될 수 있다.Modifications and variations may be made to the disclosed embodiments without departing from the spirit of the invention as defined in the following claims. For example, the central nozzle 56 may be replaced by the shower head form of a gas distributor having multiple outlets or circular arrays of gas outlets. Similarly, nozzles 34, 34a or 56a may be replaced by a ring or ring shaped structure having a gas outlet or hole through which process gas is delivered into chamber 18. Although separate nozzles 34 and 34a are preferred, a single set of nozzles 34 can be used to supply silane and SiF 4 rather than oxygen. The hole 76 may include a number of small openings arranged in a circular shape near the central nozzle 56 rather than as an annular ring. In addition, the oxygen source 71 and the third gas source 58 may be switched such that the source 71 is connected to the nozzle 56 and the source 58 is connected to the passage 70.
부가적으로, 실란, 산소 및 SiF4이외의 가스가 사용될 수 있다. 테트라에틸옥시실란(TEOS)과 같은 다른 실리콘 소스, N2O와 같은 다른 산소 소스, 및 C2F6,CF4등과 같은 플루오르 소스가 사용될 수 있다. 또한, 본 발명의 챔버는 다른 할로겐 도핑된 막, USG 막, 낮은 k 탄소막 등을 증착하는데 사용될 수 있다. 이런 실시예의 일부, 예를 들어 낮은 k 탄소막이 증착되는 실시예에서, 산소는 처리 가스로 포함될 수 없다. 그러므로, 질소와 같은 다른 가스가 이런 실시예에서 구멍(76)을 통해 유입될 것이다. 이런 동등물과 대안은 본 발명의 범위내에 포함될 수 있다고 간주된다. 이상에서는 본 발명의 양호한 일 실시예에 따라 본 발명이 설명되었지만, 첨부된 청구 범위에 의해 한정되는 바와 같은 본 발명의 사상을 일탈하지 않는 범위 내에서 다양한 변형이 가능함은 본 발명이 속하는 기술 분야의 당업자에게는 명백하다.In addition, gases other than silane, oxygen and SiF 4 may be used. Other silicon sources such as tetraethyloxysilane (TEOS), other oxygen sources such as N 2 O, and fluorine sources such as C 2 F 6 , CF 4 and the like can be used. In addition, the chambers of the present invention can be used to deposit other halogen doped films, USG films, low k carbon films, and the like. In some of these embodiments, for example embodiments in which a low k carbon film is deposited, oxygen may not be included as the process gas. Therefore, other gases, such as nitrogen, will enter through the holes 76 in this embodiment. It is contemplated that such equivalents and alternatives may be included within the scope of the present invention. Although the present invention has been described above in accordance with one preferred embodiment of the present invention, various modifications may be made without departing from the spirit of the present invention as defined by the appended claims. It is obvious to those skilled in the art.
본 발명은 각각의 가스에 대한 최적 흐름 속도의 사용과 결합되는 가스의 균일한 분배가 막에 걸쳐 균일하게 낮은 유전 상수를 초래하여 낮은 유전 상수를 가진 유전체 막을 제공한다.The present invention provides a dielectric film with a low dielectric constant whereby a uniform distribution of gases combined with the use of an optimum flow rate for each gas results in a uniformly low dielectric constant across the film.
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US20030056900A1 (en) | 2003-03-27 |
JPH10321613A (en) | 1998-12-04 |
US20050150454A1 (en) | 2005-07-14 |
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US6070551A (en) | 2000-06-06 |
US6416823B2 (en) | 2002-07-09 |
US7413627B2 (en) | 2008-08-19 |
TW380279B (en) | 2000-01-21 |
US20010053423A1 (en) | 2001-12-20 |
US6833052B2 (en) | 2004-12-21 |
US20020160113A1 (en) | 2002-10-31 |
EP0877410A1 (en) | 1998-11-11 |
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